TY - GEN
T1 - Enhanced condensation of ethylene glycol on three-dimensional pin-fin tubes
AU - Ali, Hafiz Muhammad
AU - Ali, Hassan
AU - Briggs, Adrian
PY - 2010
Y1 - 2010
N2 - New experimental data are reported for condensation of ethylene glycol at near atmospheric pressure and low velocity on six three-dimensional pin-fin tubes. Enhancements of the vapour-side, heat-transfer coefficients were found between 3 to 5.5 when compared to a plain tube at the same vapour-side temperature difference. Heat-transfer enhancement was found to be strongly dependent on the active surface area i.e. on the proportion of the tube and pin surface not covered by condensate retained by surface tension. For all the tubes, vapour-side, heat-transfer enhancements were found to be approximately 3 times the corresponding active-area enhancements. The best performing pin-fin tube gave a heat-transfer enhancement of up to 5.5; 17 % higher than those obtained from 'optimised' two-dimensional fin-tubes reported in the literature and about 24 % higher than the 'equivalent' two-dimensional integral-fin tube (i.e. with same fin root diameter, longitudinal fin spacing and thickness and fin height).
AB - New experimental data are reported for condensation of ethylene glycol at near atmospheric pressure and low velocity on six three-dimensional pin-fin tubes. Enhancements of the vapour-side, heat-transfer coefficients were found between 3 to 5.5 when compared to a plain tube at the same vapour-side temperature difference. Heat-transfer enhancement was found to be strongly dependent on the active surface area i.e. on the proportion of the tube and pin surface not covered by condensate retained by surface tension. For all the tubes, vapour-side, heat-transfer enhancements were found to be approximately 3 times the corresponding active-area enhancements. The best performing pin-fin tube gave a heat-transfer enhancement of up to 5.5; 17 % higher than those obtained from 'optimised' two-dimensional fin-tubes reported in the literature and about 24 % higher than the 'equivalent' two-dimensional integral-fin tube (i.e. with same fin root diameter, longitudinal fin spacing and thickness and fin height).
UR - http://www.scopus.com/inward/record.url?scp=84860514599&partnerID=8YFLogxK
U2 - 10.1115/IHTC14-22110
DO - 10.1115/IHTC14-22110
M3 - Conference contribution
AN - SCOPUS:84860514599
SN - 9780791849378
T3 - 2010 14th International Heat Transfer Conference, IHTC 14
SP - 11
EP - 17
BT - 2010 14th International Heat Transfer Conference, IHTC 14
ER -